WO1992009706A1 - Biodesulfuration de combustibles a base de bitume - Google Patents

Biodesulfuration de combustibles a base de bitume Download PDF

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Publication number
WO1992009706A1
WO1992009706A1 PCT/US1991/008702 US9108702W WO9209706A1 WO 1992009706 A1 WO1992009706 A1 WO 1992009706A1 US 9108702 W US9108702 W US 9108702W WO 9209706 A1 WO9209706 A1 WO 9209706A1
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Prior art keywords
bitumen
emulsion
process according
water
reaction
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James M. Valentine
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Priority to JP4502933A priority Critical patent/JP3002899B2/ja
Priority to EP92902759A priority patent/EP0558682B1/fr
Priority to CA002096736A priority patent/CA2096736C/fr
Priority to DE69129588T priority patent/DE69129588T2/de
Publication of WO1992009706A1 publication Critical patent/WO1992009706A1/fr
Anticipated expiration legal-status Critical
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    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G32/00—Refining of hydrocarbon oils by electric or magnetic means, by irradiation, or by using microorganisms
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P3/00—Preparation of elements or inorganic compounds except carbon dioxide

Definitions

  • the invention relates to the desulfurization of carbonaceous fuels by microorganisms. More particularly, the invention enables the removal of sulfur by biotechnical means from emulsified fuels containing bitumen and water.
  • bitumen-in-water emulsions have provided renewed interest in burning vast stores of viscous hydrocarbons, variously called bitumen, native bitumen, tar, natural asphalt, viscous crude oil and heavy crude. See in this regard the paper Evaluation of Handling & Combustion Characteristics of A Bitumen- in-Water Emulsified Fuel in a Commercial Utility Boiler presented in December 1989 by Blair A. Kennedy at the Power-Gen '89 Conference. See also, U.S. Patent No. 4,618,348 to M. E. Hayes et al .
  • One commercially available bitumen-in-water emulsion product, known as Ori ulsion is made with about 70% Venezuelan Orinoco crude and about 30% water. Reserves of Orinoco crude are estimated at 1.2 trillion barrels, but it typically has high sulfur and vanadium contents which deter widespread commercialization.
  • the removal of sulfur is desirable to limit the emissions of S0 ⁇ compounds to the atmosphere during combustion. These compounds are known to contribute to the formation of acid rain. Removal of contaminants prior to combustion is particularly advantageous due to the concentrated form of these contaminants prior to their reaction with oxygen to form SO ⁇ compounds during combustion.
  • the removal of SO ⁇ compounds by post-combustion methods involves the treatment of higher molecular weight compounds entrained in high-temperature, high-volume flue gases and requires that substantial capital and operating costs be applied to each major source of combustion.
  • Pre-combustion removal of contaminants has the advantage of being conducted on the preoxidized state of the contaminant and may be conducted at any point in the fuel handling and distribution stream prior to combustion.
  • Pre-combustion treatment methods may involve physical, chemical or biological treatment. Unfortun ⁇ ately, the offending sulfur compounds cannot be removed physically, and chemical treatment requires large investments in capital and high operating costs due to the use of hydrogen, solvents or the like.
  • the invention provides a simple and effective solution to the problems associated with sulfur in bitumen, thereby making large quantities of fuel available for use in the production of power and for other purposes without sacrificing environmental or economic objectives.
  • the invention provides a process for desulfurizing bitumen, comprising: contacting an emulsion of bitumen and water with a microbiological desulfurization agent selected from the group consisting of cell cultures, immobilized cell masses, fragmented cells, cell extracts, enzyme mixtures, synthetically prepared copies of active enzyme sequences or components, and mixtures of these; and, maintaining contact for a time and under conditions effective to reduce the oxidizable sulfur content of the bitumen.
  • the emulsions are preferably of the bitumen-in-water type. Following reaction, at least a portion of the original sulfur content of the bitumen has been converted to sulfates which concentrate in the aqueous phase of the emulsion.
  • the treated fuel can be treated to remove these sulfates from SO ⁇ -creating combustion reactions by either physically separating these materials or rendering them chemically incapable of the offending reactions by the addition of a suitable chemical agent during or following the reaction.
  • the Figure is a schematic flow diagram showing several alternative process schemes according to the invention.
  • the process of the invention provides a simple and effective solution to the problems associated with sulfur in bitumen.
  • the process comprises contacting an emulsion of bitumen and water with a microbiological desulfurization agent and maintaining contact for a time and under conditions effective to reduce the oxidizable sulfur content of the bitumen.
  • the treated fuel can be treated to remove these sulfates from SO ⁇ -creating combustion reactions by either physically separating these materials or rendering them chemically incapable of the offending reactions by the addition of a suitable chemical agent during or following the reaction.
  • bitumens derived from any source, including the fields known to produce such in North America, Mexico, Venezuela or the Middle East.
  • These bitumens typically have high densities, with API gravities as low as 10 degrees and less, e.g. about 7 to about 9 degrees API.
  • Sulfur contents of up to 5% are not uncommon, and of from 1 to 4% are typical.
  • This can be present in the form of inorganic and/or organic sulfur, and the present invention can be employed to facilitate the treatment of bitumen such that the SO ⁇ -potential of either or both is reduced.
  • the bitumen can be passed to an emulsifier 10 which can be any device effective for the purpose.
  • the emulsions are preferably of the bitumen-in-water type.
  • Bitumenous hydrocarbons because of their highly viscous nature, typically require extraordinary means to remove them from wells.
  • water and surfactants sometimes with steam
  • the emulsions are pumped to the surface where the emulsions of bitumen in water are broken (typically by heating under pressure) separated into bitumen and water phases, and reemulsified such as in emulsifier 10.
  • Emulsions of Orinoco crude are commercially available under the trademark Orimulsion. These are stable bitumen-in-water emulsions and do not normally require ree ulsification prior to processing according to the invention. This is, however, not a rigid rule, and there may be reason, for example, for removing at least a portion of the water phase and replacing it with one more compatible with the objectives of this invention.
  • the bitumen can be emulsified through the addition of any amount of water effective to for the emulsion. Typically, from 30 to 70% water (by volume of the final emulsion) is added (as by line 12) and the bitumen (added by line 14) is thoroughly and finely dispersed therein. Where greater amounts of water are desired (up to about 10 times these amounts, e.g., 2 to 5 times) , it may be more efficient to add only a portion prior to emulsification, and simply blend in the remainder later.
  • Effective dispersion is achieved by suitable devices, such as rotary (e.g., centrifugal pumps) , mechanical, or static, dynamic or other emulsifying devices.
  • suitable devices such as rotary (e.g., centrifugal pumps) , mechanical, or static, dynamic or other emulsifying devices.
  • the bitumen is heated to a fluid state prior to emulsification.
  • Any one of a number of known chemical or biological surfactants can be added to ensure the stability of the bitumen-in-water emulsion, with water being the continuous phase.
  • droplet sizes effective to provide a high surface area of contact between the desulfurization agent and the bitumen during reaction. This is important to both the reaction rate and to the degree of reaction which can be achieved since reactions take place at the bitumen-water interface. Fine dispersion helps to maximize the chance that the sulfur content of the individual bitumen droplets will be contacted by the desulfurization agent during the entire reaction period. It is preferred to obtain mean droplet sizes below about 250 microns, and more preferably in the range of 10 to 100 microns. This size range allows effective surface area for reaction while also assuring stability of the emulsion at reasonable energy input and surfactant levels.
  • less than 5% of the droplets will be in excess of 100 microns, and preferably this will be kept to less than 2%. While it is conceivable that desulfurization agents could be added to the aqueous phase during preparation of the oil-in-water emulsion, it is preferable that the emulsion be passed to a separate desulfurization zone, shown as 20 in the Figure, such as by line 16.
  • microbiological desul ⁇ furization agent such as via line 22
  • a microbiological desul ⁇ furization agent which can be any biological organism, living or dead, any biologically- produced enzyme or sequence of enzymes, cellular matter of an organism, or chemically-synthesized equivalent that is capable of reacting with the sulfur in the bitumen, preferably by oxidizing it to sulfate.
  • microbiological desulfurization agents are those selected from the group consisting of cell cultures, immobilized cell masses, fragmented cells, cell extracts, enzyme mixtures, synthetically-prepared copies of active enzyme sequences or components, and mixtures of these.
  • the preferred agents are capable of cleaving carbon-sulfur bonds in bitumen, and particularly in emulsion form.
  • the preferred desulfurization agents react with the bitumens such that the organic sulfur contained in them is released to the aqueous phase of the preferred bitumen-in-water emulsions. While a mixture of agents can be employed, to act on inorganic and organic sulfur with the modest utilization of carbon, the more preferred agents do not substantially affect the heating value of the fuel, but selectively oxidize organic sulfur to water-soluble sulfates which can either be physically removed or chemically bound so that they do not cause SO ⁇ production during combustion. It is, indeed, a -li ⁇
  • the reaction is conducted in any suitable reaction vessel or containment device 20 by maintaining contact between the desulfurization agent and the bitumen for a time and under conditions effective to reduce the oxidizable sulfur content of the bitumen.
  • the desulfuri ⁇ zation zone can include storage, transport or intermediate processing vessels (including pipelines) as long as conditions are maintained to sustain microorganism or other agent activity. Nutrients are added as necessary to support the growth of microorganisms. Similarly, the pH is adjusted as necessary and aeration such as via line 24 and sparging apparatus 26 may be used to serve as a supply of oxygen and/or carbon dioxide for the microorganisms. In addition to mixing by gas sparging, it is also desired to provide additional mixing shear to better distribute the gas within the reaction vessel and to reduce any tendency for gas bubbles to inhibit the reaction.
  • the reaction will be continued for a period of time sufficient to at least partially desulfurize the bitumen. Generally, time periods of under 120 days, e.g. less than 30 days will usually be adequate. There is typically no need to continue the reaction for this long. Conversely, there is usually no reason to stop the reaction at any particular time where the organisms do not degrade other aspects of the fuel. More typical reaction times will be encompassed in the range of from about 10 hours to about 300 hours of contact.
  • the contact of the bitumen with the organisms desirably results in a bitumen with a sulfur content of less than two percent and preferably one percent or less.
  • the emulsion can be at least partially broken to produce a separable aqueous layer containing the ma ority of the desulfurization agent and sulfate oxidation products.
  • the aqueous layer can then be separated from the bitumen, and the bitumen then reemulsified.
  • EET During biochemical desulfurization, sulfur is transferred from the bitumen to the aqueous phase of the emulsion.
  • the emulsion can be passed via line 28 to a separation zone 30 wherein separation is accomplished using known emulsion breaking techniques including the use of pressure, temperature, settling, centrifugation, chemical deemulsifiers or any combination. This results in the separation of desulfurized bitumen from the water, sulfates and organisms.
  • the bitumen can be withdrawn as via line 32 for storage, reemulsification, refining, or burning.
  • water treatment agents such as alkaline calcium, magnesium, aluminum, barium, and like metal compounds such as the oxides, hydroxides, and carbonates in effective amounts will eliminate the need to break the emulsion for the purpose of removing the sulfur metabolites, such as sulfates.
  • These and other treatment agents are employed to chemically bind the sulfates thereby removing them from SO ⁇ formation. They can also be added in excess of sulfate such that SO ⁇ produced by unreacted sulfur is neutralized. These agents can be employed stagewise to most effectively react with the sulfates in solution.
  • Magnesium-containing treatment agents e.g.
  • magnesium oxide and magnesium hydroxide have the desirable added advantage of decreasing problems associated with vanadium. It is also possible to add these or other agents in the form of organic salts, such as the soluble salts of calcium, magnesium, or sodium with organic acids such as formic, acetic, propionic, butyric, and the like.
  • the reaction is carried out in a plurality of stages, e. g. from 2 to 10, and typically less than 5.
  • stages e. g. from 2 to 10, and typically less than 5.
  • the reaction is brought to partial completion, the emulsion is at partially broken, and the bitumen is worked effectively (separately or during reemulsification) to bring a fresh layer of sulfur compounds to the surfaces of the individual droplets.
  • Reaction conditions, other than time will closely follow those for single stage reactions.
  • the cell culture is saved for reuse in a subsequent reaction or reaction stage, but is treated as by maceration or other known technique to obtain a cell extract which is then employed alone or in combination with another desulfuri ⁇ zation agent for a subsequent reaction or reaction stage.
  • This technique is especially advantageous when used to prepare a fuel emulsion which can be burned directly. It has the further benefit of economy while diminishing the possibility of perpetuating a contaminated culture.
  • the aqueous phase can be withdrawn from the separation zone and passed such as by line 34 to a separate sulfate removal zone 40.
  • the aqueous phase may be first treated, such as by floculation and/or filtration, to remove any cellular or other suspended material.
  • the cellular material may be reused in cellular form or as an extract.
  • the desulfurized bitumen can then be withdrawn such as by line 32 and stored, burned, reemulsified or refined. Desirably, in the case of very heavy bitumens such as
  • Orinoco bitumens and others can be reemulsified as a desulfurized oil-in-water emulsion to assist in its storage and handling.
  • it can be prepared as an oil-in-water emulsion fuel for combustion or further treatment.
  • Combustion of heavy oil-in-water emulsions is well known to those skilled in the art, and may require modifications to burner nozzles to optimize combustion. It is an advantage of the invention that when Orimulsion fuel emulsions are treated by the process of this invention, they can very easily be employed to replace coal with reduced SO ⁇ and particulates.
  • the aqueous phase in zone 40 contains microorganisms, water and sulfur.
  • the sulfur can be removed by the addition of a calcium, magnesium, aluminum or barium based water treatment/precipitating agent. Separation of the precipitated sulfates can be made at line 42 and the water and microorganisms can be recycled back to the desulfuri ⁇ zation step via conduit 44. If excess or unwanted organisms have evolved, then they can be directed as a waste stream for combustion or disposal. It is possible that new or regenerated organisms may need to be added to the recycle stream to replace those eliminated or killed in the overall process.
  • This example describes the desulfurization of Orimulsion bitumen-in-water emulsion.
  • An open barrel containing 30 gallons of emulsion is employed as the reactor.
  • the barrel is held in a vat of water which is controlled to maintain the temperature at about 30"C.
  • a sparging ring is positioned at the bottom of the barrel to deliver air into the emulsion at a rate of 100 liters per minute.
  • the emulsion has the following analysis:
  • a culture is prepared as in U.S. Patent No. 4,632,906.
  • the organism (ATCC No. 39909) is a strain of Bacillus ⁇ ulfasportare which has the ability to oxidize organic sulfur to water-soluble sulfates and utilize carbon dioxide as its sole source of carbon.
  • the aqueous phase of the emulsion is supplemented with minerals to sustain the growth of the culture and 1 liter of culture (containing 10 9 cells per milliliter) is added to the reactor. Reaction is continued for 30 days with continued air sparging gently to agitate and supply of oxygen and carbon dioxide to sustain the reaction.
  • the aqueous phase is analyzed daily for pH and sulfate.
  • the reaction mixture is manually agitated twice daily with a large paddle to minimize the problems with channeling and poor distribution of oxygen to the culture.
  • Magnesium carbonate is added as necessary to maintain the pH between 6 and 8.
  • the fuel is burned in this form without removal of the cells or sulfate salts, simply straining prior to atomization by steam or air to assure that the injection nozzles are not clogged.
  • the sulfates are bound by the magnesium and not available for the formation of SO ⁇ .
  • Example 1 The process of Example 1 is repeated, but this time the sulfur content of the emulsion is determined prior to reaction, and a stoichiometric amount of finely-divided dolomite is admixed with the emulsion at the beginning of the reaction. Periodic additions of magnesium carbonate are not employed.
  • Example 1 The process of Example 1 is again varied, this time the emulsion is transferred to a large vat after reaction and is there flooded with 300 gallons of water at 30 degrees Celcius. This treatment at least partially breaks the emulsion, permitting an aqueous layer to be decanted and the mass of live cells to be recovered. The resulting bitumen layer is then reheated and reemulsified.
  • Example 5 The process of Example 3 is repeated, but this time after separating the aqueous layer and recovering the live cells, calcium hydroxide is added in 10% excess of the sulfate to precipitate the sulfate as calcium sulfate which can be recovered and employed in the manufacture of gypsum products.
  • Example 5
  • Example 3 The process of Example 3 is again repeated, but this time the recovered cells are macerated to prepare an extract.
  • Example 1 Ten gallons of Orimulsion fuel emulsion are placed in a reactor as in Example 1, to this are added: (1) an additional fifteen gallons of water, (2) calcium carbonate, in stoiciometric amount with the sulfur in the fuel, and (3) a cell extract as prepared in example 5. The reaction is then carried out as in Example 1.
  • Example 9 The process of Example 7 is repeated but this time the emulsion is transferred to a pressure vessel following reaction and heated to about 110"C to break the emulsion. The phases are separated and the bitumen is reemulsified with sufficient water to provide an emulsion with 30% water.
  • Example 9
  • Example 7 The procedure for Example 7 is repeated, but this time employing a culture of Bacillus sphaericu IGTS9, an additional five gallons of water is added before the reaction, no magnesium carbonate is added during reac ⁇ tion, and following reaction calcium hydroxide is added to the reaction mixture in stoiciometric quantity with the original sulfur content of the fuel.
  • Example 7 The process of Example 7 is repeated, but this time the organism is B. ⁇ phaericus IGTS9, the emulsion is broken chemically following reaction, and the aqueous phase is separated and treated with alumina trihydrate.
  • Example 10 The process of Example 10 is repeated, but this time an additional ten gallons of water are added prior to the reaction, and the reaction is carried out in three stages, each of ten days duration. After each stage, the emulsion is broken by heat and pressure and the bitumen reemulsified with a fresh aqueous phase. Following the third stage reaction, the water for emulsification is reduced to three gallons.
  • Example 12
  • Example 11 The process of Example 11 is repeated, but this time the emulsion is preliminarily broken by causing pressure drop through a ball valve with exit to an open vat wherein at least a portion of the live cells are recovered for use in subsequent processing.
  • Example 1 The process of Example 1 is repeated, but this time employing a mixed culture of B. sphaericus IGTS9 and B. Sulfasportare ATCC 39909 and following reaction, adding a stoiciometric amount of alumina trihydrate based on the original sulfur content of the fuel.
  • Example 13 The process of Example 13 is repeated wherein the emulsion is then broken after reaction, the cells are separated from the aqueous phase prior to addition of the alumina trihydrate and the bitumen is reemulsified to achieve an emulsion containing 30% water.
  • Example 1 The process of Example 1 is repeated with several variations.
  • the emulsion is contacted with Rhodococcus rhodochrous IGTS8, again for thirty days and again at 30°C.
  • the reaction mixture is transferred to a large vat and is there flooded with 300 gallons of water at 30 degrees Celcius. This treatment at least partially breaks the emulsion, permitting an aqueous layer to be decanted and the mass of live cells to be recovered.
  • the water phase is then reacted with a twenty percent excess of calcium oxide to precipitate the sulfates.
  • the resulting bitumen layer is then reheated and reemulsified.

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
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  • Wood Science & Technology (AREA)
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  • Genetics & Genomics (AREA)
  • Biotechnology (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)
  • Working-Up Tar And Pitch (AREA)
  • Liquid Carbonaceous Fuels (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

Processus biochimique simple et efficace permettant de résoudre les problèmes associés au sulfure dans le bitume, par l'extraction du soufre de manière à en éliminer le rôle actif dans les réactions de combustion produisant du SOx. Une émulsion de bitume et d'eau est mise en contact avec un agent de désulfuration microbiologique pendant une durée de temps et dans des conditions permettant de réduire la teneur en soufre oxydable du bitume. Les agents préférés n'affectent pas la valeur calorifique du bitume, mais oxydent sélectivement le soufre organique en sulfates solubles dans l'eau, qui peuvent soit être extraits physiquement soit être liés chimiquement de manière à ne pas provoquer de dégagement de SOx. On utilise une réaction en plusieurs étapes pour accroître l'extraction du soufre.
PCT/US1991/008702 1990-11-21 1991-11-20 Biodesulfuration de combustibles a base de bitume Ceased WO1992009706A1 (fr)

Priority Applications (4)

Application Number Priority Date Filing Date Title
JP4502933A JP3002899B2 (ja) 1990-11-21 1991-11-20 ビチューメン燃料のバイオ脱硫
EP92902759A EP0558682B1 (fr) 1990-11-21 1991-11-20 Biodesulfuration de combustibles a base de bitume
CA002096736A CA2096736C (fr) 1990-11-21 1991-11-20 Biodesulfuration de bitume
DE69129588T DE69129588T2 (de) 1990-11-21 1991-11-20 Bioentschwefelung von bitumen-brennstoffen

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US61661090A 1990-11-21 1990-11-21
US616,610 1990-11-21

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WO1992009706A1 true WO1992009706A1 (fr) 1992-06-11

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PCT/US1991/008702 Ceased WO1992009706A1 (fr) 1990-11-21 1991-11-20 Biodesulfuration de combustibles a base de bitume

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EP (1) EP0558682B1 (fr)
JP (1) JP3002899B2 (fr)
AT (1) ATE167235T1 (fr)
CA (1) CA2096736C (fr)
DE (1) DE69129588T2 (fr)
WO (1) WO1992009706A1 (fr)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5358869A (en) * 1990-01-05 1994-10-25 Institute Of Gas Technology Microbial cleavage of organic C-S bonds
US5387523A (en) * 1991-03-15 1995-02-07 Energy Biosystems Corporation Multistage process for deep desulfurization of fossil fuels
US5472875A (en) * 1991-05-01 1995-12-05 Energy Biosystems Corporation Continuous process for biocatalytic desulfurization of sulfur-bearing heterocyclic molecules
US5529930A (en) * 1990-12-21 1996-06-25 Energy Biosystems Corporation Biocatalytic process for reduction of petroleum viscosity
EA000284B1 (ru) * 1996-03-12 1999-02-25 Эниричерке С.П.А. Штамм микроорганизма arthrobacter sp., используемый для избирательного извлечения серы из ископаемого топлива, и способ избирательного извлечения органической серы из ископаемого топлива

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6808919B2 (en) * 2002-03-11 2004-10-26 Intevep, S.A. Biodesulfurization of hydrocarbons
US7338795B2 (en) * 2002-03-11 2008-03-04 Intevep, S.A. Biodesulfurization of hydrocarbons

Citations (3)

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Publication number Priority date Publication date Assignee Title
US2975103A (en) * 1956-04-06 1961-03-14 Exxon Research Engineering Co Bacteriological desulfurization of petroleum
US4618348A (en) * 1983-11-02 1986-10-21 Petroleum Fermentations N.V. Combustion of viscous hydrocarbons
US4886519A (en) * 1983-11-02 1989-12-12 Petroleum Fermentations N.V. Method for reducing sox emissions during the combustion of sulfur-containing combustible compositions

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5132219A (en) * 1990-02-28 1992-07-21 Institute Of Gas Technology Enzymes from Rhodococcus rhodochrous strain ATCC No. 53968, Bacillus sphaericus strain ATCC No. 53969 and mixtures thereof for cleavage of organic C--S bonds of carbonaceous material

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2975103A (en) * 1956-04-06 1961-03-14 Exxon Research Engineering Co Bacteriological desulfurization of petroleum
US4618348A (en) * 1983-11-02 1986-10-21 Petroleum Fermentations N.V. Combustion of viscous hydrocarbons
US4886519A (en) * 1983-11-02 1989-12-12 Petroleum Fermentations N.V. Method for reducing sox emissions during the combustion of sulfur-containing combustible compositions
US4618348B1 (fr) * 1983-11-02 1990-05-01 Petroleum Fermentations

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
Journal of Chemical Tech. Biotechnology, Volume 48, issued 1990, LEE et al, "Sulfur Removal from Coal Through Multiphase Media Containing Biocatalysts", pages 71-79, see the Abstract. *

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5358869A (en) * 1990-01-05 1994-10-25 Institute Of Gas Technology Microbial cleavage of organic C-S bonds
US5529930A (en) * 1990-12-21 1996-06-25 Energy Biosystems Corporation Biocatalytic process for reduction of petroleum viscosity
US5387523A (en) * 1991-03-15 1995-02-07 Energy Biosystems Corporation Multistage process for deep desulfurization of fossil fuels
US5472875A (en) * 1991-05-01 1995-12-05 Energy Biosystems Corporation Continuous process for biocatalytic desulfurization of sulfur-bearing heterocyclic molecules
EA000284B1 (ru) * 1996-03-12 1999-02-25 Эниричерке С.П.А. Штамм микроорганизма arthrobacter sp., используемый для избирательного извлечения серы из ископаемого топлива, и способ избирательного извлечения органической серы из ископаемого топлива

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JPH06503119A (ja) 1994-04-07
CA2096736A1 (fr) 1992-05-22
CA2096736C (fr) 2003-02-04
EP0558682A1 (fr) 1993-09-08
ATE167235T1 (de) 1998-06-15
JP3002899B2 (ja) 2000-01-24
DE69129588T2 (de) 1999-02-18
EP0558682A4 (fr) 1994-03-09
DE69129588D1 (de) 1998-07-16
EP0558682B1 (fr) 1998-06-10

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